Process for production of electric energy and CO

1. A process for production of electric energy and CO 2 from a hydrocarbon feedstock comprising steam reforming of the feedstock producing synthesis gas, wherein the synthesis gas is separated into a hydrogen rich and carbon lean stream and a rest stream, said hydrogen rich and carbon lean stream is combusted with compressed air for producing a combustion product which is expanded in a turbine generating electric energy, said rest stream is recirculated as fuel that feeds to a combustion unit for producing heat for said steam reforming, wherein a stream comprising oxygen is fed to an oxygen adsorbing material creating an oxygen lean stream, wherein said fuel is combusted with oxygen released from said oxygen adsorbing material, thereby creating a CO 2 rich combustion product.

2. The process according to claim 1 , wherein the process further comprises at least partly converting CO and H 2 O present in the synthesis gas into CO 2 and H 2 before separating the synthesis gas.

3. The process according to claim 1 , wherein the process further comprises feeding an air stream to an air separation unit, thereby creating a first stream with an increased oxygen content and a second essentially nitrogen containing stream and feeding said first stream to the oxygen adsorbing material and mixing at least part of said second stream with said hydrogen rich stream before combustion.

4. The process according to claim 3 , wherein the process further comprises catalytically combusting at least part of said second stream together with a part of said hydrogen stream to generate a first essentially oxygen free nitrogen stream comprising some water and mixing said first essentially oxygen free nitrogen stream with the rest of said hydrogen stream.

5. The process according to claim 1 , wherein the process further comprises catalytically combusting at least part of said oxygen lean stream together with a part of said hydrogen steam to generate a second essentially oxygen free nitrogen stream comprising some water and mixing said second essentially oxygen free nitrogen stream with the rest of said hydrogen stream.

6. The process according to claim 1 , wherein the separation of the synthesis gas is obtained by pressure swing adsorption producing said rest stream at a pressure between 1-20 bar.

7. The process according to claim 1 , wherein at least a part of said oxygen lean stream is expanded in said turbine for generating electric energy.

8. The process according to claim 3 , wherein at least a part of said second essential nitrogen containing stream is expanded in said turbine for generating electric energy.

9. The process according to claim 1 , wherein said CO 2 rich combustion product is expanded in a CO 2 /H 2 O turbine for generating electric energy.

10. The process according to claim 9 , further comprising combustion of uncombusted fuel in said CO 2 rich combustion product.

11. The process according to claim 1 , wherein the separation of the synthesis gas is obtained by pressure swing adsorption producing said rest stream at a pressure between 1.5-5 bar.

12. An electric power plant comprising a steam reformer with an inlet for a hydrocarbon feedstock including one or more of water and steam and a synthesis gas outlet, said synthesis gas outlet is in communication with a hydrogen separation unit having a hydrogen rich and carbon lean stream outlet and a rest stream outlet, said hydrogen rich and carbon lean stream outlet is in communication with a combustion chamber for combusting hydrogen with compressed air having an outlet connected to a turbine for generating electric power, said rest stream outlet is in communication with a combustion unit heat-transferringly connected to said steam reformer, wherein the electric power plant plant further comprises an oxygen adsorbing material arranged inside the combustion unit, wherein said combustion unit comprises an inlet for an oxygen containing stream and an oxygen lean stream outlet and an exhaust outlet for a CO 2 rich exhaust stream.

13. The electric power plant according to claim 12 , wherein the electric power plant plant further comprises a shift unit for at least partly converting CO and H 2 O present in the synthesis gas into CO 2 and H 2 arranged upstream from the hydrogen separation unit.

14. The electric power plant according to claim 12 , wherein the electric power plant plant further comprises an air separation unit with an air inlet, an oxygen enriched stream outlet in communication with said inlet for oxygen containing stream and a nitrogen rich stream outlet in communication with said combustion chamber for combusting hydrogen.

15. The electric power plant according to claim 14 , wherein the electric power plant further comprises a low temperature stimulated combustion unit comprising an inlet in communication with said nitrogen rich stream outlet and with said hydrogen rich and carbon lean stream outlet and comprising an outlet in communication with said combustion chamber for combusting hydrogen.

16. The electric power plant according to claim 12 , wherein the electric power plant further comprises a low temperature stimulated combustion unit comprising an inlet in communication with said oxygen lean stream outlet and with said hydrogen rich and carbon lean stream outlet and comprising an outlet in communication with said combustion chamber for combusting hydrogen.

17. The electric power plant according to claim 12 , wherein said oxygen lean stream outlet is in communication with an inlet to said turbine for generating electricity.

18. The electric power plant according to claim 12 , wherein said nitrogen rich stream outlet is in communication with an inlet to said turbine for generating electricity.

19. The electric power plant according to claim 12 , wherein CO 2 rich exhaust stream is in communication with a CO 2 /H 2 O turbine that generates electricity.